A mass and charge balance (MCB) model that can simulate oxide growth and dissolution kinetics simultaneously during corrosion of an alloy has been recently developed. In this study, the MCB model was applied to the corrosion of the Co-Cr alloy Stellite-6. The construction of the model and the assignment of values to the rate parameters for the model are presented. The model simulation results are then compared with experimental corrosion data collected as a function of pH, temperature and polarization potential. The data include the current during potentiostatic polarization, the corrosion potential under open-circuit conditions, and post-test analyses of the oxide formed and the amount of metal dissolved. Excellent agreement between the model results and experimental data are found. This is evidence that the MCB model is a useful tool for predicting time-dependent corrosion while an oxide film is evolving. Alloys owe their corrosion resistance to protective oxide films formed on their surfaces. [1][2][3][4][5][6][7][8][9][10][11][12][13][14][15][16][17] Corrosion involves surface redox reactions (metal oxidation coupled with solution reduction) and interfacial transfer of the charged species involved in the redox reactions. The presence of an oxide film hinders the interfacial charge transfer, slowing the rate of corrosion. Modeling oxide formation and growth as a function of the solution environment is an important component in predicting the corrosion behavior of an alloy.Several corrosion models have been developed for predicting the rate of oxide growth 11,18-31 and/or the rate of metal dissolution in the presence of an oxide film. To obtain the overall rate of corrosion, many of these models focus on solving the transport rate equations for individual charge carriers (interstitial cations and anions, cation and anion vacancies, and electrons and holes) across the oxide film, in addition to the rates of their creation at respective interfaces (i.e. electrochemical redox reaction rates). These models assign rates to the transport of different charge carriers that are difficult to verify. Since the rate of interfacial charge transfer depends on the electric field present at the interface, the electrochemical potentials of the alloy, the oxide and the solution phases are important parameters in determining the corrosion rate.Many of the existing models acknowledge that the driving force for corrosion depends on the potential of the corroding system (the corrosion potential (E corr ) in an open circuit or the applied potential (E app ) during polarization). However, these models do not specifically quantify the driving force as a function of electrode potential and/or other quantifiable potentials such as the equilibrium potential of a redox pair involved in corrosion (E eq rdx ). The electrode potential and the redox pair may change with time as corrosion progresses. The nature of oxide and the oxide layer structure can also change with time as corrosion progresses even under potentiostatic polarization or con...